US4309282AExpiredUtilityPatentIndex 89
Process of phosphate ore beneficiation in the presence of residual organic polymeric flocculants
Est. expiryApr 14, 2000(expired)· nominal 20-yr term from priority
B03D 2201/002B03D 1/016B03D 2201/02B03D 1/008B03D 1/021B03D 2203/06B03D 1/012
89
PatentIndex Score
31
Cited by
9
References
6
Claims
Abstract
Froth flotation of phosphate ore in the presence of residual organic polymeric flocculants is improved in recovery when a collector comprising a fatty acid derived from vegetable or mineral oils and a surface active agent is employed.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1. A process for the froth flotation of phosphate values from an aqueous ore pulp containing about 0.1 to 5 parts per million of residual organic polymer flocculants which comprises: conditioning said ore pulp with from about 0.1 to 5.0 pounds of collector per ton of ore, said collector comprising, in combination, from about 99.0 to 1.0 weight percent of a fatty acid derived from vegetable or animal oils and, correspondingly, from about 1.0 to 99.0 weight percent of a surface active agent wherein the surface active agent is either a partial polycarboxylic acid ester of the general structure: ##STR13## wherein R 2 is a linear or branched radical having from 8 to 23 carbon atoms, inclusive, n is an integer of from 0 to 8 inclusive, p is an integer of from 0 to 8 inclusive, wherein n+p is equal to or greater than (1) and R 1 is a bivalent grouping selected from --CH 2 --m wherein m is an integer of 1 to 6, --CH═CH, ##STR14## --C 6 H 8 --, and C 6 H 10 --, or is a sulfosuccinamate of the general structure: ##STR15## wherein R 2 is a linear or branched, saturated or unsaturated radical having from 8 to 23 carbon atoms, inclusive, and X is selected from the group consisting of hydrogen, sodium, potassium and ammonium and thereafter froth floating the phosphate values.
2. The process of claim 1 wherein from about 0.5 to about 2.0 pounds of collector per ton of ore is employed.
3. The process of claim 1 wherein the collector comprises from about 95.0 to 80.0 weight percent of a fatty acid and, correspondingly, from about 5.0 to 20.0 weight percent of a surface active agent.
4. The process of claim 1 wherein the fatty acid employed in the collector is derived from tall oil.
5. The process of claim 1 wherein the partial polycarboxylic acid ester employed in the collector is one in which R 2 is a linear or branched aliphatic radical having 11 to 15 carbon atoms, inclusive.
6. The process of claim 1 wherein the partial polycarboxylic acid ester employed in the collector is of the structure: ##STR16##Cited by (0)
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